Optimal modes of side-section flow in heat-pump-assisted extractive distillation systems for separating allyl alcohol–allyl acetate mixtures with butyl propionate
https://doi.org/10.32362/2410-6593-2021-16-3-213-224
Abstract
Objectives. To investigate the influence of side-section flow modes on the energy efficiency of a partially thermally coupled distillation sequence (PTCDS) with a vapor recompression heat pump for the extractive distillation of an allyl alcohol–allyl acetate mixture with n-butyl propionate and identify modes under which the combined use of a PTCDS and heat pump are the most efficient.
Methods. Mathematical modeling in the Aspen Plus V10 software package was used as the main research method. The local composition equation of the non-random two-liquid model was used as a model for describing the vapor–liquid equilibrium, while the Redlich–Kwong model was used to consider the non-ideal vapor phase. When modeling the conventional extractive distillation scheme and PTCDS, parametric optimization was carried out according to the criterion of the total energy costs in the column reboilers. For the economical evaluation, Aspen Process Economic Analyzer V10.1 tools were used.
Results. For extractive distillation of a mixture of allyl alcohol (30 wt %) and allyl acetate (70 wt %) with n-butyl propionate as an entrainer, the minimum energy consumption was achieved at the same side-section flow mode for the variants of a PTCDS with and without a heat pump. The reduction in energy costs relative to the conventional scheme was 20% for the sequence without a heat pump and 38% for that with a heat pump. An economic assessment was made of the best options in comparison with the conventional extractive distillation scheme. The PTCDS with a heat pump had an advantage over the sequence without a heat pump only for long periods of operation.
Conclusions. For the extractive distillation of an allyl alcohol–allyl acetate mixture, the optimal modes for the combined use of a PTCDS with a vapor recompression heat pump coincide with the optimal modes for a PTCDS without a heat pump.
Keywords
About the Authors
P. S. KlauznerRussian Federation
Pavel S. Klauzner, Assistant, Department of Chemistry and Technology of Basic Organic Synthesis
86, Vernadskogo pr., Moscow, 119571
ResearcherID AAJ-7842-2021
D. G. Rudakov
Russian Federation
Danila G. Rudakov, Cand. Sci. (Eng.), Associate Professor, Department of Chemistry and Technology of Basic Organic Synthesis
86, Vernadskogo pr., Moscow, 119571
Scopus Author ID 37018548000
ResearcherID M-5241-2014
E. A. Anokhina
Russian Federation
Elena A. Anokhina, Cand. Sci. (Eng.), Associate Professor, Department of Chemistry and Technology of Basic Organic Synthesis
86, Vernadskogo pr., Moscow, 119571
Scopus Author ID 6701718055
ResearcherID E-5022-2016
A. V. Timoshenko
Russian Federation
Andrey V. Timoshenko,Dr. Sci. (Eng.), Professor, Department of Chemistry and Technology of Basic Organic Synthesis
86, Vernadskogo pr., Moscow, 119571
Scopus Author ID 56576076700
ResearcherID Y-8709-2018
References
1. Grigoriev A.A., Katsman E.A. Allylacetate and Syntheses on Its Basis. Kataliz i neftekhimiya = Catalysis and Petrochemistry. 2001;7:27–39 (in Russ.).
2. Anokhina E.A., Kardona K., Pisarenko Y.A., Saksonova O.I., Ponomarev V.N. The main stages of the combined processes development on the example of NSRRP for the production of allyl alcohol by butanolysis of allyl acetate. Part 1. Khim. Prom. = Chem. Ind. 1996;9:3–9 (in Russ.).
3. Anokhina E.A., Kardona K., Pisarenko Y.A., Saksonova O.I., Ponomarev V.N. The main stages of the combined processes development on the example of NSRRP for the production of allyl alcohol by butanolysis of allyl acetate. Part 2. Khim. Prom. = Chem. Ind. 1996;11:689–693 (in Russ.).
4. Klauzner P.S., Rudakov D.G., Anokhina E.A., Timoshenko A.V. Application of a complex with patricianly coupled thermal and energy flows and heat pumps in extractive distillation of allyl alcohol–allyl acetate mixture with n-butylpropionate. Chem. Technol. of Org. Subst. 2020;4(16):42–56 (in Russ.).
5. You X., Rodriguez-Donis I., Gerbaud V. Improved design and efficiency of the extractive distillation process for acetone–methanol with water. Ind. Eng. Chem. Res. 2015;54(1):491–501. https://doi.org/10.1021/ie503973a
6. Luyben W.L. Distillation column pressure selection. Sep. Purif. Technol. 2016;168:62–67. https://doi.org/10.1016/j.seppur.2016.05.015
7. Luyben W.L. Control of heat-integrated extractive distillation processes. Comp. Chem. Eng. 2018;111:267–277. https://doi.org/10.1016/j.compchemeng.2017.12.008
8. Tiverios P.G., van Brunt V. Extractive distillation solvent characterization and shortcut design procedure for methylcyclohexane–toluene mixtures. Ind. Eng. Chem. Res. 2000;39(6):1614–1623. https://doi.org/10.1021/ie990654k
9. Petlyuk F.B., Serafimov L.A. Mnogokomponentnaya rektifikatsiya. Teoriya i raschet (Distillation of Multicomponent Mixtures. Theory and Calculation). Moscow: Khimiya; 1983. 304 p. (in Russ.).
10. Petlyuk F.B., Platonov B.M., Slavinskii D.M. The thermodynamic optimal methods of separation of multicomponent mixtures. Khim. Prom. = Chem. Ind. 1965;3:206–211 (in Russ.).
11. Timoshenko A.V., Morgunov A.V., Anokhina E.A. Flowsheet synthesis for extractive distillation of azeotropic mixtures in systems consisting of columns with partially coupled heat and material flows. Theor. Found. Chem. Eng. 2007;41(6):845–850. https://doi.org/10.1134/S0040579507060097 [Original Russian Text: Timoshenko A.V., Morgunov A.V., Anokhina E.A. Flowsheet synthesis for extractive distillation of azeotropic mixtures in systems consisting of columns with partially coupled heat and material flows. Teor. Osnovy Khim. Tekhnol. 2007;41(6):649–655 (in Russ.).]
12. Anokhina E.A. Energy saving in extractive distillation. Vestnik MITHT (Tonk. Khim. Tekhnol. = Fine Chem. Technol.) 2013;8(5):3–19. (in Russ.).
13. Wang C., Guang C., Cui Y., Wang C., Zhang Z. Compared novel thermally coupled extractive distillation sequences for separating multi-azeotropic mixture of acetonitrile/benzene/methanol. Chem. Eng. Res. Des. 2018;136:513–528. https://doi.org/10.1016/j.cherd.2018.06.017
14. Gutierrez-Guerra R., Segovia-Hernández J.G., Hernandez S., Bonilla-Petriciolet A., Hernández H. Design and Optimization of Thermally Coupled Extractive Distillation Sequences. Comp. Aid. Chem. Eng. 2009;26:189–194. https://doi.org/10.1016/S1570-7946(09)70032-X
15. Yang A., Sy Y., Chien I.L., Jin S., Yan C., Wei S., Shen W., et al. Investigation of an energy-saving double-thermally coupled extractive distillation for separating ternary system benzene/toluene/cyclohexane. Energy. 2019;186:115756. https://doi.org/10.1016/j.energy.2019.07.086
16. Anokhina E., Timoshenko A. Criterion of the energy effectiveness of extractive distillation in the partially thermally coupled columns. Chem. Eng. Res. Des. 2015;99:65–175. https://doi.org/10.1016/j.cherd.2015.03.006
17. Anokhina E.A., Timoshenko A.V., Akishin A.Y., Remizova A.V. Benzene purification from thiophene using dimethylformamide as an entrainer in thermally coupled extractive distillation columns. Chem. Eng. Res. Des. 2019;146(5):391–403. https://doi.org/10.1016/j.cherd.2019.04.003
18. Gerbaud V., Rodriguez-Donis I., Hegelyc L., Langc P., Denis F., Youe X.Q. Review of extractive distillation. Process design, operation, optimization and control. Chem. Eng. Res. Des. 2019;141:229–271. https://doi.org/10.1016/j.cherd.2018.09.020
19. You X., Rodriguez-Donis I., Gerbaud V. Reducing process cost and CO2 emissions for extractive distillation by double-effect heat integration and mechanical heat pump. App. Energy. 2016;166:128–140. https://doi.org/10.1016/j.apenergy.2016.01.028
20. Luo H., Bildea C.S., Kiss A.A. Novel Heat-pumpassisted extractive distillation for bioethanol purification. Ind. Eng. Chem. Res. 2015;54(7):2208–2213. https://doi.org/10.1021/ie504459c
21. Wang C., Zhuang Y., Liu L., Zhang L., Du J. Heat pump assisted extractive distillation sequences with intermediateboiling entrainer. App. Therm. Eng. 2021;186:116511. https://doi.org/10.1016/j.applthermaleng.2020.116511
22. Gu J., You X., Tao C., Li J. Analysis of heat integration, intermediate reboiler and vapor recompression for the extractive distillation of ternary mixture with two binary azeotropes. Chem. Eng. Process. 2019;142:107546. https://doi.org/10.1016/j.cep.2019.107546
23. Aurangzeb Md., Jana A.K. Vapor recompression with interreboiler in a ternary dividing wall column: Improving energy efficiency and savings, and economic performance. App. Therm. Eng. 2018;147:1009–1023. https://doi.org/10.1016/j.applthermaleng.2018.11.008
24. Timoshenko A.V., Anokhina E.A., Rudakov D.G., Timofeev V.S., Tatsievskaya G.I., Matyushenkova Yu.V. Power saving in distillation using complexes with coupled flows. Vestnik MITHT (Tonk. Khim. Tekhnol. = Fine Chem. Technol.) 2011;6(4):28–39 (in Russ.).
25. Plesu V., Bonet-Ruiz A.E., Bonet J., Llorens J. Simple equation for suitability of heat pump use in distillation. Comp. Aided Chem. Eng. 2014;33:1327–1332. https://doi.org/10.1016/B978-0-444-63455-9.50056-8
26. Patraşcu I., Bildea C. S., Kiss A. A. Eco-efficient Downstream Processing of Biobutanol by Enhanced Process Intensification and Integration. ACS Sustain. Chem. Eng. 2018;6(4):5452–5461. https://doi.org/10.1021/acssuschemeng.8b00320
27. Shi P., Zhang Q., Zeng A., Ma Y., Yuan X. Eco-efficient vapor recompression-assisted pressure-swing distillation process for the separation of a maximum-boiling azeotrope. Energy. 2020;196(13):117095. https://doi.org/10.1016/j.energy.2020.117095
28. Reay D.A., Macmichael D. Heat pumps. Design and applications. UK: Pergamon Press; 1979. 302 р.
29. Kiss A.A., Ferreira C.A. Heat Pumps in Chemical Process Industry. US-FL: CRC Press; 2016. 442 р. https://doi.org/10.1201/9781315371030
Supplementary files
|
1. PTCDS heat duty, PTCDS with HP reduced heat duty, and side flow dependence on side-stream stage. | |
Subject | ||
Type | Исследовательские инструменты | |
View
(160KB)
|
Indexing metadata ▾ |
|
2. This is to certify that the paper titled Optimal modes of side-section flow in heat-pump-assisted extractive distillation systems for separating allyl alcohol–allyl acetate mixtures with butyl propionate commissioned to us by Pavel S. Klauzner, Danila G. Rudakov, Elena A. Anokhina, and Andrey V. Timoshenko has been edited for English language and spelling by Enago, an editing brand of Crimson Interactive Inc. | |
Subject | CERTIFICATE OF EDITING | |
Type | Other | |
View
(428KB)
|
Indexing metadata ▾ |
- For the extractive distillation of the allyl alcohol–allyl acetate mixture with butyl propionate as an entrainer, containing 30 wt % of allyl alcohol, the co-use of a partially thermally coupled distillation sequence (PTCDS) with vapor recompression heat pumps was considered;
- The influence of side section flow modes on the energy efficiency of a PTCDS with vapor recompression heat pump was investigated. The minimum energy consumption was achieved at the same mode of side section flow both for the variant of a PTCDS with and without a heat pump;
- An economic analysis for the most energy efficient variants of schemes showed that the co-use of the PTCDS with vapor recompression heat pumps in the extractive distillation of the considered mixture was economically feasible only with a long service life.
Review
For citations:
Klauzner P.S., Rudakov D.G., Anokhina E.A., Timoshenko A.V. Optimal modes of side-section flow in heat-pump-assisted extractive distillation systems for separating allyl alcohol–allyl acetate mixtures with butyl propionate. Fine Chemical Technologies. 2021;16(3):213-224. https://doi.org/10.32362/2410-6593-2021-16-3-213-224